CN2706216Y - Double section multieffect distilled water machine - Google Patents
Double section multieffect distilled water machine Download PDFInfo
- Publication number
- CN2706216Y CN2706216Y CN 200420040651 CN200420040651U CN2706216Y CN 2706216 Y CN2706216 Y CN 2706216Y CN 200420040651 CN200420040651 CN 200420040651 CN 200420040651 U CN200420040651 U CN 200420040651U CN 2706216 Y CN2706216 Y CN 2706216Y
- Authority
- CN
- China
- Prior art keywords
- water
- effect
- evaporator
- inlet pipe
- water inlet
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Landscapes
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
The utility model provides a double section multi-effect distilled water machine, belonging to the water distillation equipment field. The double section multi-effect distilled water machine comprises successive each effect connecting evaporator, connecting pipelines and valves which are matched with each effect connecting evaporator. The utility model is characterized in that each effect evaporator is composed of an evaporation section of the upper part and a steam-water separating section of the lower part. A raw material water intake pipe (3) is arranged inside each effect evaporator, and the opening of the intake pipe is positioned in the bottom of each effect evaporator. The utility model adopts the structure that the intake pipe enters the evaporator from the bottom, so the pipe pass of the outboard exposed pipeline of the machine is shortened, and the dissipation of the heat quantity is decreased. The raw material water also can be preheated by the steam with high temperature inside the evaporator body, the utilization of heat quantity is improved, and the yield result of the distilled water is improved largely in the end.
Description
Technical field
The utility model belongs to water distillation equipment field, specifically is a kind of two section type multi-effect water distillator.
Background technology
At present, the equipment of producing medical distilled water generally adopts multi-effect water distillator.This distillation machine is serially connected by multi-effect evaporator, its structure of evaporimeter that the prior art distillation machine adopts mostly is external inlet channel, and evaporimeter is the top water inlet, like this when each single-effect evaporator connects successively, because its water inlet pipe mouth is at the top of evaporimeter, the water inlet pipe of each single-effect evaporator all prolongs on the bottom to the top, must will extending so make use of momentum, each exposes tube side at the water inlet pipe of device external, the device external pipeline is barish many more, scattering and disappearing of heat is just big more, the utilization rate of heat is just low more, the most directly cause the reduction greatly of energy waste and distilled water productive rate, how can solve similar problem, to become industry technical staff's a problem.
The utility model content
The purpose of this utility model is to overcome above-mentioned deficiency of the prior art, provide a kind of raw water water inlet pipe to be arranged on the inside of each single-effect evaporator, and simple and compact for structure, heat scatters and disappears little, the heat utilization ratio height, the two section type multi-effect water distillator that the distilled water yield is high.
The utility model is achieved through the following technical solutions:
It is a kind of two section type multi-effect water distillator, comprise each single-effect evaporator that connects successively and the duct coupling that matches, valve, it is characterized in that each single-effect evaporator that is adopted is made of for two sections the evaporator section on top and the carbonated drink segregation section of bottom, raw water water inlet pipe (3) is arranged on the inside of each single-effect evaporator, and water inlet pipe mouth (20) is positioned at each single-effect evaporator bottom.
The top of described evaporator evaporation section is cloth water chamber (23), and water inlet pipe (3) is set in the cloth water chamber (23), and this water inlet pipe (3) runs through vaporiser body downwards, and water inlet pipe mouth (20) is visited the outside that reaches vaporiser body.For ease of processing, water inlet pipe 3 can be positioned at the center of vaporiser body, and water inlet pipe 3 tops can be higher than water distributing plate 13 upper surfaces of each tubulation group 15 top.
The utility model is because the structure that has adopted water inlet pipe to enter vaporiser body from the bottom, also just shortened the equipment tube side of exposed pipeline outward, reduced scattering and disappearing of heat, make simultaneously raw water in vaporiser body by the high-temperature steam preheating, improve the utilization rate of heat, so can finally improve producing effects of distilled water greatly.
Description of drawings
Below in conjunction with accompanying drawing the utility model is described in further detail:
Fig. 1: the utility model mounting structure example structure schematic diagram.
Fig. 2: evaporimeter example structure schematic diagram.
The specific embodiment
The utility model is installed standby according to prior art as shown in Figure 1, each water inlet pipe 3 can be all enters the evaporimeter inner chamber from the bottom of evaporimeter, various like this pipelines are arranged on the bottom of each single-effect evaporator mostly, have shortened the tube side of exposed pipeline greatly, make structure more compact.
Before use, the admission mouth of pipe 22 with first evaporator connects with Industrial Boiler vapour source by pipeline 10 earlier, and raw material water inlet pipe 3 connects with the water source by pump and valve, and in a usual manner electric apparatus control apparatus is installed.
It is cloth water chamber 23 that the utility model adopts the top of evaporator evaporation section, water inlet pipe 3 is set in the cloth water chamber 23, this water inlet pipe 3 runs through vaporiser body downwards, water inlet pipe mouth 20 is visited the outside that reaches vaporiser body, for ease of processing, water inlet pipe 3 can be positioned at the center of vaporiser body, and water inlet pipe 3 tops can be higher than water distributing plate 13 upper surfaces of each tubulation group 15 top.
In use, throw the hot industry Boiler Steam into for the evaporation cavity 14 of first evaporator 9 by steam inlet pipe 22, the steam of high temperature is soon to tubulation group 15 heat temperature raisings, raw water is successively through condenser 6 simultaneously, preheater 11 enters the water inlet pipe mouth 20 that is positioned at base of evaporator, and inject cloth water chamber 23 fast, the water distributing plate 13 of raw water through all planting the water through hole flows in each tubulation of tubulation group 15 then, and in each tubulation by high speed carburetion, raw water after the vaporization is descending fast always, carrying the raw water that is not vaporized fully secretly and entering into steam-water separation chamber through steam-water separator 18, at the Zhong Shui of steam-water separation chamber, after vapour separates, clean high temperature, high steam separates once more through carbonated drink separate mesh 19, enters into steam inlet pipe 22 evaporation cavities 14 of lower effective evaporator at last along venthole 17; Condensed lustration raw material water just coagulates water pipe 21 from raw material discharges, and enters into the water inlet pipe mouth 20 of lower effective evaporator, successively UNICOM.The Boiler Steam water of condensation in first evaporator evaporation cavity 14 is just discharged from delivery port 16 and is entered preheater 11, give the heating of the raw water in the raw material water inlet pipe 3 that from preheater 11, passes, simultaneously because each single-effect evaporator raw water water inlet pipe 3 is built-in, so raw water is preheated once more in evaporimeter, the drain valve that condensed Boiler Steam water is provided with on preheater 11 in the preheater 11 that first evaporator links emits, and the preheater 11 of follow-up each single-effect evaporator links successively.Last evaporator 4 and with it the steam in the preheater of UNICOM be the distilled water steam of cleaning, so it links by pipeline 2,1 and condenser 6 respectively, after the condensation of condenser 6, collect by outlet pipe 5, for improving the cooling effect of condenser 6, in the condenser 6 cool cycles water pipe 7,8 can be set, cool for condenser 6 by the effect of circulating pump.
In addition, the built-in structure of the water inlet pipe that the utility model adopted promptly is suitable for the evaporimeter of structure shown in Figure 2, also is applicable to the evaporimeter of other steam-water separation structure forms.
The utility model is because the structure that has adopted water inlet pipe to enter evaporimeter from the bottom, so shortened the equipment tube side of exposed pipeline outward, reduced scattering and disappearing of heat, also can make simultaneously raw water in vaporiser body by the high-temperature steam preheating, improve the utilization rate of heat, so can finally improve producing effects of distilled water greatly.
Claims (4)
1, a kind of two section type multi-effect water distillator, comprise each single-effect evaporator that connects successively and the duct coupling that matches, valve, it is characterized in that each single-effect evaporator that is adopted is made of for two sections the evaporator section on top and the carbonated drink segregation section of bottom, raw water water inlet pipe (3) is arranged on the inside of each single-effect evaporator, and water inlet pipe mouth (20) is positioned at each single-effect evaporator bottom.
2, two section type multi-effect water distillator according to claim 1, the top that it is characterized in that described evaporator evaporation section is cloth water chamber (23), water inlet pipe (3) is set in the cloth water chamber (23), this water inlet pipe (3) runs through vaporiser body downwards, and water inlet pipe mouth (20) is visited the outside that reaches vaporiser body.
3, two section type multi-effect water distillator according to claim 2 is characterized in that water inlet pipe (3) is positioned at the center of vaporiser body.
4, two section type multi-effect water distillator according to claim 1 is characterized in that water inlet pipe (3) top is higher than water distributing plate (13) upper surface of each tubulation group (15) top.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200420040651 CN2706216Y (en) | 2004-05-20 | 2004-05-20 | Double section multieffect distilled water machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200420040651 CN2706216Y (en) | 2004-05-20 | 2004-05-20 | Double section multieffect distilled water machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2706216Y true CN2706216Y (en) | 2005-06-29 |
Family
ID=34850639
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200420040651 Expired - Fee Related CN2706216Y (en) | 2004-05-20 | 2004-05-20 | Double section multieffect distilled water machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2706216Y (en) |
-
2004
- 2004-05-20 CN CN 200420040651 patent/CN2706216Y/en not_active Expired - Fee Related
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| WO2021213552A1 (en) | Multi-column differential pressure energy-saving anhydrous alcohol distillation system and anhydrous alcohol energy-saving production method | |
| CN106766342A (en) | Ammonia still process column overhead ammonia vapour residual heat system is reclaimed using lithium bromide absorption type heat pump | |
| CN207276237U (en) | A kind of high energy-saving type thermocompression distiller | |
| WO2008138212A1 (en) | Multitower energysaving distillation system | |
| CN2706216Y (en) | Double section multieffect distilled water machine | |
| CN203196362U (en) | High-efficient alcohol recovery tower | |
| CN208959348U (en) | A kind of evaporation concentration device of feed liquid | |
| CN100404095C (en) | Double distillation type multiple-effect distilled water machine | |
| CN115155088B (en) | Rectifying device for KL540 crystallization processing and application method thereof | |
| CN110407272A (en) | A kind of hot pressing multi-effect water distillator and its working method | |
| CN2705219Y (en) | Double section type screen separating evaporator | |
| CN108662915A (en) | The indirect heat exchange vaporization type condensing system of the general vapour of concentration evaporator system end effect | |
| CN205627127U (en) | MVR triple -effect evaporator | |
| CN2726696Y (en) | Composite type Chinese medicinal liquid concentrating and alcohol reclaiming device | |
| CN109297010B (en) | Power equipment condensate water recovery system with water vapor compressor | |
| CN209138027U (en) | A kind of waste heat recycling VOC condensate recovery system | |
| CN106830150A (en) | A kind of economic benefits and social benefits solar water purifier and its process for preparing water | |
| CN2779072Y (en) | Condensation device for high gas content gas-steam mixture of direct air cooling units | |
| CN208998343U (en) | A kind of Separated self-control adjusting boiler smoke condenser | |
| CN2705220Y (en) | Double section screw separating evaporator | |
| CN206624665U (en) | A kind of economic benefits and social benefits solar water purifier | |
| CN2730453Y (en) | Double distillation type multi-functional distilled water apparatus | |
| CN107583300B (en) | A kind of hypergravity MVR heat pump rectification system | |
| CN206320954U (en) | Ammonia still process column overhead ammonia vapour residual heat system is reclaimed using lithium bromide absorption type heat pump | |
| CN100368046C (en) | Raising membrane distributing water type evaporator |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20050629 Termination date: 20130520 |